CN204251459U - A kind of water treatment production line - Google Patents
A kind of water treatment production line Download PDFInfo
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- CN204251459U CN204251459U CN201420499241.0U CN201420499241U CN204251459U CN 204251459 U CN204251459 U CN 204251459U CN 201420499241 U CN201420499241 U CN 201420499241U CN 204251459 U CN204251459 U CN 204251459U
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- XLYOFNOQVPJJNP-UHFFFAOYSA-N water Substances O XLYOFNOQVPJJNP-UHFFFAOYSA-N 0.000 title claims abstract description 193
- 238000004519 manufacturing process Methods 0.000 title claims abstract description 33
- 239000008399 tap water Substances 0.000 claims abstract description 26
- 235000020679 tap water Nutrition 0.000 claims abstract description 26
- 238000003776 cleavage reaction Methods 0.000 claims abstract description 18
- 239000000693 micelle Substances 0.000 claims abstract description 16
- 238000002407 reforming Methods 0.000 claims abstract description 16
- 239000011159 matrix material Substances 0.000 claims abstract description 11
- 239000000945 filler Substances 0.000 claims abstract description 10
- 239000012530 fluid Substances 0.000 claims abstract description 4
- 239000000463 material Substances 0.000 claims description 19
- OKTJSMMVPCPJKN-UHFFFAOYSA-N Carbon Chemical compound [C] OKTJSMMVPCPJKN-UHFFFAOYSA-N 0.000 claims description 16
- 230000000249 desinfective effect Effects 0.000 claims description 7
- 239000002253 acid Substances 0.000 claims description 6
- 238000005245 sintering Methods 0.000 claims description 6
- 238000005520 cutting process Methods 0.000 claims description 4
- 230000001954 sterilising effect Effects 0.000 claims description 4
- CBENFWSGALASAD-UHFFFAOYSA-N Ozone Chemical compound [O-][O+]=O CBENFWSGALASAD-UHFFFAOYSA-N 0.000 claims description 3
- 238000004659 sterilization and disinfection Methods 0.000 claims description 3
- 229910052500 inorganic mineral Inorganic materials 0.000 abstract description 22
- 239000011707 mineral Substances 0.000 abstract description 22
- 238000011049 filling Methods 0.000 abstract description 11
- 238000007781 pre-processing Methods 0.000 abstract description 8
- 238000010276 construction Methods 0.000 abstract description 3
- 238000000034 method Methods 0.000 description 17
- 229910001220 stainless steel Inorganic materials 0.000 description 15
- XEEYBQQBJWHFJM-UHFFFAOYSA-N Iron Chemical compound [Fe] XEEYBQQBJWHFJM-UHFFFAOYSA-N 0.000 description 10
- 238000000108 ultra-filtration Methods 0.000 description 10
- 239000000843 powder Substances 0.000 description 8
- 239000007788 liquid Substances 0.000 description 7
- 238000002156 mixing Methods 0.000 description 7
- 229910052613 tourmaline Inorganic materials 0.000 description 7
- 229940070527 tourmaline Drugs 0.000 description 7
- 239000011032 tourmaline Substances 0.000 description 7
- 239000007921 spray Substances 0.000 description 6
- 239000010935 stainless steel Substances 0.000 description 6
- 229910052742 iron Inorganic materials 0.000 description 5
- XKRFYHLGVUSROY-UHFFFAOYSA-N Argon Chemical compound [Ar] XKRFYHLGVUSROY-UHFFFAOYSA-N 0.000 description 4
- 239000002131 composite material Substances 0.000 description 4
- 238000010586 diagram Methods 0.000 description 4
- 238000009776 industrial production Methods 0.000 description 4
- 239000003610 charcoal Substances 0.000 description 3
- 238000007599 discharging Methods 0.000 description 3
- 230000000694 effects Effects 0.000 description 3
- 238000005516 engineering process Methods 0.000 description 3
- 239000011152 fibreglass Substances 0.000 description 3
- 238000011010 flushing procedure Methods 0.000 description 3
- 239000011521 glass Substances 0.000 description 3
- 239000001257 hydrogen Substances 0.000 description 3
- 229910052739 hydrogen Inorganic materials 0.000 description 3
- 238000002360 preparation method Methods 0.000 description 3
- 238000006057 reforming reaction Methods 0.000 description 3
- 230000029058 respiratory gaseous exchange Effects 0.000 description 3
- 238000005070 sampling Methods 0.000 description 3
- 238000013022 venting Methods 0.000 description 3
- 238000003466 welding Methods 0.000 description 3
- VYPSYNLAJGMNEJ-UHFFFAOYSA-N Silicium dioxide Chemical compound O=[Si]=O VYPSYNLAJGMNEJ-UHFFFAOYSA-N 0.000 description 2
- 229910000831 Steel Inorganic materials 0.000 description 2
- 230000004913 activation Effects 0.000 description 2
- 229910052786 argon Inorganic materials 0.000 description 2
- 229960000892 attapulgite Drugs 0.000 description 2
- HSJPMRKMPBAUAU-UHFFFAOYSA-N cerium(3+);trinitrate Chemical compound [Ce+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O HSJPMRKMPBAUAU-UHFFFAOYSA-N 0.000 description 2
- 239000004927 clay Substances 0.000 description 2
- 238000004590 computer program Methods 0.000 description 2
- 230000005611 electricity Effects 0.000 description 2
- 230000004907 flux Effects 0.000 description 2
- FYDKNKUEBJQCCN-UHFFFAOYSA-N lanthanum(3+);trinitrate Chemical compound [La+3].[O-][N+]([O-])=O.[O-][N+]([O-])=O.[O-][N+]([O-])=O FYDKNKUEBJQCCN-UHFFFAOYSA-N 0.000 description 2
- 230000005415 magnetization Effects 0.000 description 2
- 238000012856 packing Methods 0.000 description 2
- 229910052625 palygorskite Inorganic materials 0.000 description 2
- 238000002203 pretreatment Methods 0.000 description 2
- 238000012545 processing Methods 0.000 description 2
- 150000003384 small molecules Chemical class 0.000 description 2
- 239000010959 steel Substances 0.000 description 2
- YZCKVEUIGOORGS-UHFFFAOYSA-N Hydrogen atom Chemical compound [H] YZCKVEUIGOORGS-UHFFFAOYSA-N 0.000 description 1
- 230000031018 biological processes and functions Effects 0.000 description 1
- 238000009835 boiling Methods 0.000 description 1
- 235000020682 bottled natural mineral water Nutrition 0.000 description 1
- 238000001816 cooling Methods 0.000 description 1
- 238000009826 distribution Methods 0.000 description 1
- 238000001914 filtration Methods 0.000 description 1
- 239000007789 gas Substances 0.000 description 1
- 239000011796 hollow space material Substances 0.000 description 1
- XLYOFNOQVPJJNP-UHFFFAOYSA-M hydroxide Chemical compound [OH-] XLYOFNOQVPJJNP-UHFFFAOYSA-M 0.000 description 1
- 239000012535 impurity Substances 0.000 description 1
- 230000006698 induction Effects 0.000 description 1
- 238000009434 installation Methods 0.000 description 1
- 238000005259 measurement Methods 0.000 description 1
- 239000000203 mixture Substances 0.000 description 1
- 238000000465 moulding Methods 0.000 description 1
- 238000005457 optimization Methods 0.000 description 1
- 238000003825 pressing Methods 0.000 description 1
- 229910052761 rare earth metal Inorganic materials 0.000 description 1
- 150000002910 rare earth metals Chemical class 0.000 description 1
- 239000002994 raw material Substances 0.000 description 1
- 238000007493 shaping process Methods 0.000 description 1
- 239000002689 soil Substances 0.000 description 1
- 239000007787 solid Substances 0.000 description 1
- 230000006641 stabilisation Effects 0.000 description 1
- 238000011105 stabilization Methods 0.000 description 1
- 239000002351 wastewater Substances 0.000 description 1
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- Water Treatment By Electricity Or Magnetism (AREA)
Abstract
The utility model relates to a kind of water treatment production line, comprise connect successively treating nature water system, the first intermediate water tank, stable micro-molecular group water for system, the second intermediate water tank and conventional tap water aftertreatment systems, described first intermediate water tank is communicated with the filling preprocessing system of described conventional tap water.Described stable micro-molecular group water comprises cleavage reaction tank and reforming reactor for system, placing in described cleavage reaction tank makes macromolecular mass water resolve into the matrix material filler of small-micelle water, the motion of described reforming reactor for making fluid water do perpendicular cuts magnetic line of force.Water treatment production line of the present utility model has the ability of producing common mineral water and subset mineral water simultaneously, and production line compact construction, space utilization rationally, can save a large amount of fixing inputs.
Description
Technical field
The utility model belongs to water-treatment technology field, is specifically related to a kind of water treatment production line, can produce common mineral water and small-micelle water mineral water simultaneously.
Background technology
The current mineral water drunk for people, pure water and magnetization, purified tap water, all absorbed by body cell owing to not solving water from the molecular structure of water at all, the problem utilized, and also exist as mineral water, pure water staging life there will be owing to being in not mobility status for a long time, with the hydrogen ion (H+) of positive electricity and attract each other within the quite a while with the hydroxide ion (OH-) of negative electricity and be polymerized agglomerating situation with hydrogen bond in water molecules, lose activity and slow down and reduce tap water and be absorbed by the body, activation body etc. ensures that human body is in healthy vital water quality effect.
In most cases, particularly when long inactivity, water can form the water molecule cluster of nearly tens water moleculess.These water molecule clusters are random, a unbodied chain ball of string.Its dissolving power, seepage force are all very low, are not easily absorbed by animal, plant and people, and the water be made up of this water molecule cluster can become " one, stagnant water ".The water molecule cluster of these amorphous structures through certain physical chemistry process, can become the small-micelle water of the water molecule cluster containing less water molecules.
Have the activation and small-micelle water that water is being studied by a lot of tap water manufacturing enterprise to prepare technology at present, the method for use has a lot, comprises magnetization, high temperature, biological process, vibration etc., all can realize the object of cutting large water molecule cluster.
Current water treatment production line, general operating mine spring or small-micelle water, technical process is not quite similar, and needs through more processing step process and large quantities of relevant devices, also just means and needs to drop into a large amount of fund and needs take larger space, place.
Utility model content
The purpose of this utility model is to provide a kind of water treatment production line, is combined by small-micelle water industrial production line with common mineral water production line, makes a production line have the ability of producing common mineral water, small-micelle water mineral water simultaneously.
The technical solution adopted in the utility model is as follows:
A kind of water treatment production line, comprise connect successively treating nature water system, the first intermediate water tank, stable micro-molecular group water for system, the second intermediate water tank and conventional tap water aftertreatment systems, described first intermediate water tank is communicated with described conventional tap water aftertreatment systems.
Further, described treating nature water system is connected to form in turn by a raw water box, a more medium filter, an activated charcoal filter, an accurate filter and a ultra-violet disinfecting device.
Further, described stable micro-molecular group water is connected to form by cutting retort, an acid activated charcoal filter, a cartridge filter and a reforming reactor in turn for system.
Further, place and make macromolecular mass water resolve into the matrix material filler of small-micelle water in described cleavage reaction tank, described matrix material filler is the ball material that the activated sintering of material is formed based on tourmalinite.
Further, described matrix material filler accounts for the 70-90% of described cleavage reaction tank volume.
Further, described cleavage reaction tank is multiple, therebetween connected in series or parallel join.
Further, described reforming reactor comprises: strong magnetic generating unit, and comprise some kicker magnets, described kicker magnet forms high-intensity magnetic field in pairs; Guiding device, is placed among described high-intensity magnetic field, for the motion making fluid water do perpendicular cuts magnetic line of force.
Further, described reforming reactor is multiple, therebetween connected in series or parallel join.
Further, described conventional tap water aftertreatment systems is connected to form in turn by a subset water tank, a lift pump, a ultra-violet disinfecting device, an ozone sterilization system, a finished product water tank, a finished product water pump and an inline final filter.
Further, described first intermediate water tank and stable micro-molecular group water are respectively equipped with a lift pump between system, between described second intermediate water tank and described conventional tap water aftertreatment systems.
In water treatment production line of the present utility model, when the first intermediate water tank is communicated with the filling preprocessing system of described conventional tap water, as preparation common mineral water prepare path.First intermediate water tank and stable micro-molecular group water are for preparing path as subset mineral water during system connectivity, and therefore this production line has the ability of producing common mineral water and subset mineral water simultaneously; Micromolecular water Preparation equipment comprises cleavage reaction device and reforming reaction device, makes its stabilization for the preparation of micromolecular water.The present invention is by essence filter in adjustment small-micelle water industrial production line, ultrafiltration, sterilizing flow process, water tank, lift pump in increase, make the common mineral water production line of the parallel access of small-micelle water industrial production line, achieve a line double-purpose, achieve industrial production line and merge with item adjustment and optimization.Compared with traditional single product production line, water treatment production line compact construction of the present utility model, space utilization rationally, have been saved a large amount of fixing inputs, can have been obtained reasonable economic benefit.
Accompanying drawing explanation
Fig. 1 is the schematic diagram of the water treatment production line of the utility model embodiment.
Fig. 2 is the water treatment production line idiographic flow schematic diagram of the utility model embodiment.
Fig. 3 is the one-piece construction schematic diagram of reforming reactor in embodiment.
Fig. 4 is the structural representation of the guiding device of reforming reactor in embodiment.
Embodiment
Below by specific embodiments and the drawings, the utility model is described in detail.
Fig. 1 is the schematic diagram of the water treatment production line of the utility model embodiment, comprise connect successively treating nature water system, the first intermediate water tank, stable micro-molecular group water for system, the second intermediate water tank and conventional tap water aftertreatment systems, described first intermediate water tank is communicated with the filling preprocessing system of described conventional tap water.
Fig. 2 is the water treatment production line particular flow sheet of the present embodiment, is also plant layout figure simultaneously.As shown in the drawing, this water treatment production line comprises: be arranged in the conventional tap water pretreatment system in production plant left-half space and stable micro-molecular group water for system; Be arranged in ultrafiltration system and the conventional tap water aftertreatment systems (or claiming conventional tap water filling preprocessing system) of production plant right half part; Described conventional tap water pretreatment system and stable micro-molecular group water are for being communicated with a 1# intermediate water tank between system; Described stable micro-molecular group water is for being communicated with a 2# intermediate water tank between system and ultrafiltration system; 2# intermediate water tank is communicated with in turn with ultrafiltration system and the filling preprocessing system of conventional tap water; Be communicated with one between 1# intermediate water tank and ultrafiltration system and prepare path with stable micro-molecular group water for the common mineral water of system in parallel.
Described conventional tap water pretreatment system is connected to form in turn by a raw water box, a more medium filter, an activated charcoal filter, an accurate filter and a ultra-violet disinfecting device.Described stable micro-molecular group water is connected to form by a cutting retort group, an acid activated charcoal filter, a cartridge filter and a reforming reactor group in turn for system.The filling preprocessing system of described conventional tap water is connected to form in turn by a subset water tank, a lift pump, a ultra-violet disinfecting device, an ozone sterilization system, a finished product water tank, a finished product water pump and an inline final filter.Described 1# intermediate water tank and stable micro-molecular group water are for being provided with a lift pump between system.A lift pump is provided with between described 2# intermediate water tank and ultrafiltration system.Described common mineral water is prepared path and is provided with a ultrafiltration lift pump.
Take from the former water of natural mineral water and introduce raw water box by workshop external pipe (not shown), then flow through more medium filter, activated charcoal filter, ultrafilter and ultra-violet disinfecting device successively and carry out preliminary process, filter out impurities and sterilize, and conventional tap water pre-treatment.Water after pre-treatment enters 1# intermediate water tank.
When producing subset mineral water, water enters small-micelle water through lift pump and prepares system, flow through cleavage reaction tank group, acid activated charcoal filter, cartridge filter and reforming reactor group successively, the now small-micelle water of obtained steady state, enter 2# intermediate water tank, entering ultrafiltration system by lift pump, and then entering after the filling preprocessing system of conventional tap water processes, be delivered to filling water spot and encapsulate.
When producing common mineral water, water is prepared path by common mineral water and is arranged ultrafiltration lift pump thereon and enters ultrafiltration system, and then enters after the filling preprocessing system of conventional tap water processes, and is delivered to filling water spot and encapsulates.
The water treatment production line topology layout that the present embodiment is lifted is compact, can make full use of space, produces separately common mineral water and subset mineral water than each layout production line, can save fixed assets cost in a large number and drop into, and effectively reduce floor space.
The following describes the type selecting of some emphasis water treating equipment:
1,1# intermediate water tank:
Quantity: 1; Capacity: 10T; Specification: φ 2000 × 3800mm; Material: 304 stainless steels; Pressure: normal pressure.This intermediate water tank comprises: intake-outlet, water port, pneumostome, manhole, breathing filter, gage glass, sampling valve etc.
2, the lift pump after 1# intermediate water tank
Quantity: 1; Flow: 10m3/Hr/ platform; Pressure: 0.42Mpa; Material: stainless steel; Power: 3.0KW; Voltage: 380VAC 50HZ three-phase five-wire mode.
3, cleavage reaction tank group
Quantity: 8 covers; Specification: Φ 800 × 1800mm; Tank body material: 304 stainless steels; Control mode: multiway valve controls automatically.Each cleavage reaction tank has: stainless steel piping, valve system, intake-outlet, venting port, evacuation port, discharge opening, filler etc.
The following describes the specific implementation method of this water clusters cleavage reaction tank.
1) equipment material and mounting condition
Equipment all adopts 304 food grade stainless steels or 306 food grade stainless steels to make.Guarantee that system is placed on solid smooth horizontal base, preferably concrete foundation.System should as far as possible near drainage position.Sewerage should reach the backwash flow of 20 minutes by processing unit.Ground should smooth and level.Equipment (comprising water shoot and upflow tube) is not placed in room temperature lower than the environment of 0 DEG C.
2) pipeline connects
Hydraulic pressure should maintain more than 25psi (1.72bar), as pressure is greater than 100psi (7.88bar), pipeline should install reducing valve additional.
1. the water-in of system is connected with former water supply line, the water outlet of system is connected with follow-up supply line.When in the face of tank body adapter time, water-in should in left side.
2. be installed into outlet valve system, make system for ease of maintenaince.
3. tank body adapter is connected water shoot (drainage elbow can rotating 360 degrees, connect to facilitate pipeline).
4. water shoot is for discharging tank body internal memory liquid.Discharge pipe line length is more short better, and discharge outlet is more low better.Pipeline is not extended to more than 40 feet.If hydraulic pressure is lower than 30psi (2.1bar), water shoot discharge outlet should higher than multi-way valve body.
3) installation of valve
1. packing ring is put on valve body, and with 2 screws, packing ring is fixed;
2. valve is put on adapter, puts 10 allen screws, and tighten
4) filling of matrix material and discharging
Filler: the feeding port opening stainless steel tank deck, evenly pours into granular composite material in stainless cylinder of steel, is filled up to 80% of All Told Measurement.Close feeding port.
Discharging: open evacuation port, by the emptying of stainless cylinder of steel internal memory liquid, opens discharge opening, is drawn off by matrix material.
This matrix material also can be described as ion-sieve material, and its composition is tourmalinite, great soil group nonmetallic mineral material and rare earth material.This matrix material can adopt following method to prepare:
1) raw material is taken, each component and massfraction are respectively: the 800-1200 order iron tourmaline powder of 12-21%, the 100-400 order iron tourmaline powder of 10-16%, the 100-150nm tourmaline powder of 2-4%, the diatomite of 22-28%, the polynite of 15-20%, the attapulgite clay of 22-28%, the cerous nitrate of 0.1-0.2%, and the lanthanum nitrate of 0.1-0.2%;
2) by cerous nitrate and lanthanum nitrate mixing, and dissolve into spray-water, make mixing spray liquid;
3) by iron tourmaline powder, tourmaline powder, diatomite, polynite and attapulgite clay mixing, regulate the spray humidity of described mixing spray liquid, the powder of mixing is made spheroid under the effect of described mixing spray liquid;
4) sintering processes is carried out to described spheroid, after cooling, obtain final material.
Preferably, step 3) the spray humidity of described mixing spray liquid is 10-20%.
Preferably, step 3) granularity of described spheroid is 3-5mm.
Preferably, step 3) adopt disk machine to prepare described spheroid, its rotating speed is 130-230 rev/min.
Preferably, in described disk machine, appropriate ball core is added shaping to accelerate spheroid.
Preferably, step 4) the control temperature rise rate that adopts when sintering is 2-4 DEG C/min, sintering temperature is 700-1000 DEG C, and the time is 2-4 hour.
Preferably, step 4) adopt retort furnace to carry out described sintering,
Preferably, described iron tourmaline powder is Xinjiang iron tourmaline powder.
5) equipment runs
To fetch boiling water molecular grouping cleavage reaction tank equipment vent valve, open water intaking valve, utilize the computer program of inlet/outlet valve system to control to carry out back flushing to water clusters cleavage reaction appliance arrangement, back flushing 8 minutes.Flushing waste water enters lower ditch by vent valve.
Open evacuation port, close vent valve, utilize the computer program of inlet/outlet valve system to control just to rinse water clusters cleavage reaction appliance arrangement, just rinsing 8 minutes.Open vent valve, close evacuation port, when liquid fill tank body flow out from vent valve time, open water discharge valve, close vent valve.Equipment enters normal use.
During concrete enforcement, as required, multiple water molecule cluster cleavage reaction device machine can be carried out connected in series or parallel join, or first parallel join more connected in series.Than as shown in Figure 18 cleavage reaction tanks being connected together.
4, acid charcoal canister (containing charcoal)
Quantity: 2 covers; Specification: Φ 800 × 2200mm; Tank body material: 304 stainless steels; Control mode: multiway valve controls automatically.This acid charcoal canister comprises: stainless steel piping, valve system, intake-outlet, venting port, evacuation port, discharge opening, filler etc.Water distribution manner: large discharge slight drag is uniform.
5,5 μ ultrafilter
Quantity: 1; Material: 304 stainless steels; Filtering accuracy: 5 μm.This 5 μ ultrafilter comprises: intake-outlet, venting port, evacuation port, filter core pull bar, pressing plate, water eliminator etc.
6, reforming reactor quantity: 4 covers
Reforming reactor the water molecules of just disordered motion can carry out ordering arrangement, and form constitutionally stable small molecules cluster, this process is reforming reaction process.Concrete, this reforming reactor comprises, and the last one magnetic generating unit, comprises some kicker magnets, and described kicker magnet forms high-intensity magnetic field in pairs; One guiding device, is placed among described high-intensity magnetic field, and fluid can do the motion of perpendicular cuts magnetic line of force in guiding device; The magneticstrength of described strong magnetic generating unit is not less than 3500 Gausses; Described guiding device comprises some layers of thrust-augmenting nozzle and pipe connecting group, and individual layer thrust-augmenting nozzle is planar spiral structures; Each layer thrust-augmenting nozzle is communicated with by pipe connecting group interval, forms single path; The magnetic journey of described individual layer thrust-augmenting nozzle is 4000-10000mm.
Concrete, as shown in Figures 3 and 4, this reforming reactor comprises: 8 permanent magnets 1, and its magnetic intensity is 3500 Gausses, uses securing supports 3 to fix; Guiding device 2 comprises 7 layers of thrust-augmenting nozzle 4, and every layer of water conservancy diversion length is 4825mm, and thrust-augmenting nozzle 4 is planar spiral structures, is communicated with by pipe connecting group 5, forms single path.Permanent magnet 1 is annulus sheet, and the hollow space of pipe connecting group 5 through permanent magnet 1 and the outside from permanent magnet 1 are communicated with thrust-augmenting nozzle 4.Thrust-augmenting nozzle is stainless pipe, and described pipe connecting group is made up of stainless pipe, stainless joint and stainless pipe elbow.2 adjacent permanent magnets 1 form a high-intensity magnetic field, have one deck thrust-augmenting nozzle 4 in each high-intensity magnetic field, and the magnetic line of force of high-intensity magnetic field is perpendicular to the plane at the place, axis of thrust-augmenting nozzle 4.The small-micelle water of unsteady state flows into thrust-augmenting nozzle 4, flow out after all layers, in this process, the small-micelle water of unsteady state is in the state of perpendicular cuts magnetic line of force in individual layer water conservancy diversion 4, because high-intensity magnetic field has enough intensity and sufficiently long magnetic journey, so, can improve can in water molecules, the linear hydrogen bond state of orderly induction water molecules, changes water molecules bond angle degree and length, enhanced stability; Clustered water is formed by the characteristic of linear hydrogen bonding water molecules self-organization memory; This process is reforming reaction.Small-micelle water can be made to be in steady state for a long time.
Preferably, described kicker magnet is annular slice, and pipe connecting group passes hollow sections and the outside of kicker magnet.Preferably, also comprise some securing supports, make kicker magnet relatively fixing, make adjacent two kicker magnets form all strong high-intensity magnetic field.Preferably, described thrust-augmenting nozzle is stainless pipe, and described pipe connecting group is made up of stainless pipe, stainless pipe joint and stainless pipe elbow.Preferably, described thrust-augmenting nozzle is glass fiber reinforced plastics composite material pipe, and described pipe connecting group is made up of glass fiber reinforced plastics composite material pipe and glass fiber reinforced plastics composite material pipe elbow.
7,2# intermediate water tank
Quantity: 1; Capacity: 5T; Specification: φ 1600 × 3200mm; Material: 304 stainless steels; Pressure: normal pressure.This intermediate water tank comprises: intake-outlet, water port, pneumostome, manhole, breathing filter, gage glass, sampling valve etc.
8, the water lift pump after 2# intermediate water tank
Quantity: 1; Operating flux: 30m3/Hr overcurrent; Material: stainless steel; Pressure: 0.50Mpa; Service rating: 7.5KW; Running voltage: 380VAC 50HZ three-phase four-wire system.
9, small molecules water tank
Quantity: 1; Capacity: 5T; Specification: φ 1600 × 3200mm; Material: 304 stainless steels; Pressure: normal pressure.Comprise: intake-outlet, water port, pneumostome, manhole, breathing filter, gage glass, sampling valve etc.
10, micromolecular water lift pump
Quantity: 1; Operating flux: 30m3/Hr overcurrent material: stainless steel; Pressure: 0.42Mpa; Service rating: 5.5KW; Running voltage: 380VAC 50HZ three-phase four-wire system
11, above pipes between devices and valve
Material: 304 stainless steels; Welding process: adopt applying argon gas protection, argon arc welding welding by one side, double-side molding process.
12, other, also can comprise online measuring instrument (PH on-line detector, flow on-line detector etc.), master system (for collecting water treatment key parameter and store), electric control system etc.
Above embodiment is only in order to illustrate the technical solution of the utility model but not to be limited; those of ordinary skill in the art can modify to the technical solution of the utility model or equivalent replacement; and not departing from spirit and scope of the present utility model, protection domain of the present utility model should be as the criterion with described in claim.
Claims (7)
1. a water treatment production line, comprise connect successively treating nature water system, the first intermediate water tank, stable micro-molecular group water for system, the second intermediate water tank and conventional tap water aftertreatment systems, described first intermediate water tank is communicated with described conventional tap water aftertreatment systems;
Described stable micro-molecular group water is connected to form by cutting retort, an acid activated charcoal filter, a cartridge filter and a reforming reactor in turn for system; Placing in described cleavage reaction tank makes macromolecular mass water resolve into the matrix material filler of small-micelle water, and described matrix material filler is the ball material that the activated sintering of material is formed based on tourmalinite;
Described reforming reactor comprises: strong magnetic generating unit, and comprise some kicker magnets, described kicker magnet forms high-intensity magnetic field in pairs; Guiding device, is placed among described high-intensity magnetic field, for the motion making fluid water do perpendicular cuts magnetic line of force.
2. water treatment production line as claimed in claim 1, is characterized in that: described treating nature water system is connected to form in turn by a raw water box, a more medium filter, an activated charcoal filter, an accurate filter and a ultra-violet disinfecting device.
3. water treatment production line as claimed in claim 1, is characterized in that: described matrix material filler accounts for the 70-90% of described cleavage reaction tank volume.
4. water treatment production line as claimed in claim 1, is characterized in that: described cleavage reaction tank is multiple, therebetween connected in series or parallel join.
5. water treatment production line as claimed in claim 1, is characterized in that: described reforming reactor is multiple, therebetween connected in series or parallel join.
6. water treatment production line as claimed in claim 1, is characterized in that: described conventional tap water aftertreatment systems is connected to form in turn by a subset water tank, a lift pump, a ultra-violet disinfecting device, an ozone sterilization system, a finished product water tank, a finished product water pump and an inline final filter.
7. water treatment production line as claimed in claim 1, is characterized in that: described first intermediate water tank and stable micro-molecular group water are respectively equipped with a lift pump between system, between described second intermediate water tank and described conventional tap water aftertreatment systems.
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| Application Number | Priority Date | Filing Date | Title |
|---|---|---|---|
| CN201420499241.0U CN204251459U (en) | 2013-08-29 | 2014-08-28 | A kind of water treatment production line |
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| Application Number | Priority Date | Filing Date | Title |
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| CN201320532781X | 2013-08-29 | ||
| CN201320532781 | 2013-08-29 | ||
| CN201420499241.0U CN204251459U (en) | 2013-08-29 | 2014-08-28 | A kind of water treatment production line |
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| CN204251459U true CN204251459U (en) | 2015-04-08 |
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Cited By (1)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104230090A (en) * | 2013-08-29 | 2014-12-24 | 吉林天士力矿泉饮品有限公司 | Water treatment production line |
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2014
- 2014-08-28 CN CN201420499241.0U patent/CN204251459U/en not_active Expired - Lifetime
Cited By (2)
| Publication number | Priority date | Publication date | Assignee | Title |
|---|---|---|---|---|
| CN104230090A (en) * | 2013-08-29 | 2014-12-24 | 吉林天士力矿泉饮品有限公司 | Water treatment production line |
| CN104230090B (en) * | 2013-08-29 | 2017-10-24 | 吉林天士力矿泉饮品有限公司 | A kind of water process production line |
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